CN110841487B - Preparation method of seawater desalination membrane - Google Patents
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D71/00—Semi-permeable membranes for separation processes or apparatus characterised by the material; Manufacturing processes specially adapted therefor
- B01D71/06—Organic material
- B01D71/08—Polysaccharides
- B01D71/12—Cellulose derivatives
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- B01D67/00—Processes specially adapted for manufacturing semi-permeable membranes for separation processes or apparatus
- B01D67/0079—Manufacture of membranes comprising organic and inorganic components
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D69/00—Semi-permeable membranes for separation processes or apparatus characterised by their form, structure or properties; Manufacturing processes specially adapted therefor
- B01D69/12—Composite membranes; Ultra-thin membranes
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D71/00—Semi-permeable membranes for separation processes or apparatus characterised by the material; Manufacturing processes specially adapted therefor
- B01D71/02—Inorganic material
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D71/00—Semi-permeable membranes for separation processes or apparatus characterised by the material; Manufacturing processes specially adapted therefor
- B01D71/06—Organic material
- B01D71/08—Polysaccharides
- B01D71/10—Cellulose; Modified cellulose
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/44—Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2103/00—Nature of the water, waste water, sewage or sludge to be treated
- C02F2103/08—Seawater, e.g. for desalination
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
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- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A20/00—Water conservation; Efficient water supply; Efficient water use
- Y02A20/124—Water desalination
- Y02A20/131—Reverse-osmosis
Abstract
The invention relates to the technical field of new materials and membrane separation, and particularly discloses a preparation method of a seawater desalination membrane.
Description
Technical Field
The invention relates to the technical field of membrane separation, relates to a preparation method of a seawater desalination membrane, and particularly relates to a preparation method of a seawater desalination membrane with high desalination rate and high water flux.
Background
Of the total water in the world, ocean and salt lake water account for about 97%, land water only accounts for 3% (and is 76% occupied by glaciers), and therefore the available water resource is only 0.5%. These only fresh waters are unevenly distributed, resulting in severe water shortages in 26 countries worldwide, with 10 million people lacking safe drinking water. In addition to the shortage of water resources, the discharge amount of industrial sewage is rapidly increased with the development of industrial technology, and the resulting harm has become a serious social crisis. About four thousand and two billion tons of sewage are discharged into rivers every year all over the world, so that water pollution of fifty thousand and one billion tons of water bodies in rivers, lakes and offshore areas is caused, and the water pollution accounts for about two thirds of the total fresh water amount. The world population is expected to grow further 40-50% in the next 50 years, and with urbanization and industrialization, the demand for existing water resources will increase further. Therefore, most regions of the world face a serious shortage of fresh water resources.
Seawater desalination is mainly a process of removing impurities from water, i.e., removing particles from water and forcing water molecules to permeate through a porous medium. Currently, the main seawater desalination technologies used in industry are reverse osmosis, thermal multi-stage flash evaporation, electrodialysis and thermal multi-effect distillation. Among them, reverse osmosis is the most widely used technique for desalinating seawater because of its advantages of low energy consumption, simple operation, easy maintenance and modular equipment. Reverse osmosis membranes, although commercialized, have relatively low water flux, poor chemical stability, and short service life.
In recent years, graphene has attracted much attention as a novel two-dimensional carbon nanomaterial in the fields of physicochemical and material science due to its high specific surface area and excellent electrical, thermal, and mechanical properties. Graphene Oxide (GO) is used as a graphene derivative, and has a wide development prospect in the fields of molecular separation and desalination due to excellent molecular permeability. Because the nano-sheet layers are stacked to form a layered structure and form a nano-interlayer channel, the passing of molecules and ions at the nano scale can be screened due to the particularity of the nano-structure. The GO sheet layer contains a large number of oxygen-containing groups, so that the graphene oxide has good hydrophilic performance, and the unique nano structure forms an sp2 nano capillary network, so that ultra-fast water molecule transmembrane transmission is realized.
However, the performance of GO membranes is currently limited by the solution-diffusion mechanism, with ion sieving depending on the size of the GO layer spacing. When the GO film is placed in an aqueous solution, hydration will result in increased spacing between GO nanosheets. However, the precisely controlled reduction of GO thin films to below 0.7nm interlayer spacing and to remain unchanged during immersion is a huge challenge for GO membrane applications in the field of ion sieving and desalination. Therefore, the search for a proper reduction method to precisely regulate and control the interlayer spacing of the GO thin film and keep the interface physicochemical property and interlayer spacing unchanged in the subsequent water desalination process is the key of the GO thin film applied to the seawater desalination field.
Disclosure of Invention
Aiming at various problems of the existing materials, the invention provides a preparation method of a seawater desalination membrane, specifically, three diamine monomers with different structures are adopted to modify graphene oxide, the interlayer spacing of nanosheets is regulated and controlled to prevent GO from expanding in water between layers, then the GO is self-assembled on a mixed cellulose membrane or a cellulose acetate membrane, and finally a modified graphene oxide composite membrane is obtained.
The invention specifically comprises the following contents:
a preparation method of a seawater desalination membrane is characterized in that the seawater desalination membrane is a modified graphene oxide composite membrane, specifically, three diamine monomers with different structures are adopted to modify graphene oxide, the interlayer spacing of nanosheets is regulated and controlled to prevent GO from interlayer expansion in water, and then the graphene oxide composite membrane is self-assembled on a mixed cellulose membrane or a cellulose acetate membrane to finally obtain the modified graphene oxide composite membrane.
The method comprises the following specific steps:
(1) measuring concentrated sulfuric acid 60-100mL in a beaker, placing in a water bath, cooling with ice water and continuously stirring, adding graphite powder 0.5-5g and NaNO 0.5-3g3Slowly adding 6-20g KMnO at the temperature below 10 DEG C4Keeping the temperature at 0 ℃ for 12h-36h to promote low-temperature intercalation reaction, then placing the mixture in a constant-temperature water bath at 25-45 ℃ and keeping stirring; after 20-40min, taking out and cooling to normal temperature, diluting with 150-180ml deionized water, and continuously stirring until the system becomes brownish black; after 15min, 500mL deionized water and 30mL H at 75-95 deg.C are added2O2To remove excess oxidant; obtaining golden yellow suspension;
in the process, a large amount of bubbles can be observed to be generated in the system, meanwhile, the liquid is obviously changed from brown black to graphite oxide, the graphite oxide is graphite oxide with loose and expanded interlaminations, and the graphene oxide can be formed by interlamination fracture after the cells are crushed by the ultrasonic wave in the next step;
(2) equally dividing the suspension into centrifugal tubes, and separating the suspension by using a centrifugal machine at the rotating speed of 3000 plus 5000 revolutions to obtain a brownish red precipitate; centrifugally cleaning the precipitate for 2 times by using a dilute hydrochloric acid solution, and washing the precipitate to be neutral by water; dispersing the precipitate in water, treating the obtained suspension liquid by using a cell disruptor for 5 minutes, carrying out water bath ultrasound for 2 hours, centrifuging to obtain supernatant, and freeze-drying to obtain dry graphene oxide powder;
the graphene oxide powder prepared by the method has the advantages of mild and safe preparation conditions, no special high temperature and high pressure, simple and easily obtained experimental raw materials, and environmental friendliness. The obtained graphene oxide has high purity, relatively regular appearance, medium size and regular edges, a typical tissue packaging structure of the graphene oxide can be seen, and the prepared graphene oxide has high oxidation degree and can provide a good foundation for subsequent reaction;
(3) weighing the obtained 60-100mg of graphene oxide, putting the graphene oxide into a beaker, adding deionized water to prepare 200ml of solution, adding 0.05-0.1mol of diamine monomer cross-linking agent, uniformly stirring, putting the mixture into a water bath kettle at the temperature of 60 ℃, and continuously stirring for 6-12 hours to fully perform cross-linking reaction on the graphene oxide and the cross-linking agent;
(4) diluting the crosslinked suspension to 10mg/L by using deionized water, and passing through a mixed cellulose membrane or a cellulose acetate membrane serving as a filter in a vacuum filtration device under the fixed pressure of 0.1MPa to realize the self-assembly of the membrane, so as to obtain a modified graphene oxide composite membrane on the mixed cellulose membrane or the cellulose acetate membrane; and placing the composite membrane in an oven at 60-80 ℃ for 6-24h to promote the crosslinking reaction between the graphene oxide and the monomer, and then soaking the composite membrane in pure water for 12-24h to remove physical adhesion substances and redundant crosslinking agents, thereby obtaining the target seawater purification membrane.
In the above technical solution, the diamine monomer cross-linking agent is selected from one or more of urea, ethylenediamine or p-phenylenediamine, wherein urea or ethylenediamine is preferably used alone; the reaction mechanism of the diamine monomer crosslinker is as follows:
the graphene oxide can effectively screen metal ions due to the fact that sub-nanometer interlayer channels are easily formed by stacking of two-dimensional sheet layers of the graphene oxide, and water molecules can easily pass through the interlayer channels due to abundant hydrophilic oxygen-containing groups between the sheet layers; but the GO interlayer spacing is enlarged and unstable to cause swelling due to the influence of hydration in the solution, so that effective ion screening cannot be carried out; the deeper reason is that the GO nano-sheets have the function of delocalized and large-wandering bonds among the layers, and the bonds belong to physical bonds and have weaker strength, so that swelling occurs when water and salt ions enter, and the distance between the layers is enlarged;
the invention utilizes that the edges and the defects of graphene oxide lamella contain a large number of oxygen-containing functional groups (such as hydroxyl carboxyl and the like), the inventor selects that amino in diamine monomer can react with the oxygen-containing functional groups, and firmly fixes and connects the lamellae in a chemical bond form, thereby realizing the regulation and control of the distance between the nanosheets to prevent GO from interlayer expansion in water. In addition, the cross-linking agents used by the people are diamine monomers, and the structures of the cross-linking agents contain two amino groups, so that the cross-linking reaction between two sheet layers and one diamine monomer molecule can be realized structurally, the cross-linking regulation interlayer spacing is realized, and the salt ion exclusion at the nanometer level is realized; the diamine monomer cross-linking agent selected by the invention has the advantages that the source is wide, cheap and easily available, the cross-linking agent is green and environment-friendly, and in addition, the cross-linking agent selected by the invention contains two amino groups, so that the maximum utilization of functional groups in the cross-linking agent is realized, and the reaction can be most sufficient under the cross-linking agent with the same concentration and quality.
Meanwhile, the three crosslinking agents selected by the invention have small molecular mass, so that the three crosslinking agents can stably exist among layers and cannot prop up the interlayer distance due to self reasons. At present, most desalting membranes are organic reaction self-made organic compound membranes, different organic structures are obtained through organic compound reaction, and pores appear in the structures to obtain porous membranes. The technical scheme of the invention is that a nanostructure channel is formed by self-stacking of unique two-dimensional nano sheets of graphene oxide, and the solution permeation channels are fixedly regulated and controlled by a crosslinking reaction, so that the regulation and control of the graphene oxide nanostructure and the application in desalination are really realized, and the blank in the field is filled.
Furthermore, the inventor optimizes the preparation method, and the specific steps after optimization are as follows:
(1) measuring 80mL of concentrated sulfuric acid in a furnacePutting the cup in a water bath kettle, cooling with ice water, stirring, adding 0.5-2.5g of graphite powder and 1-1.5g of NaNO3Slowly adding 9-15g KMnO at the temperature below 10 DEG C4Keeping the temperature at 0 ℃ for 24 hours to promote low-temperature intercalation reaction, then placing the mixture in a constant-temperature water bath at 35 ℃ and keeping stirring; after 30min, taking out and cooling to normal temperature, diluting with 150-180ml deionized water, and continuously stirring, wherein the system becomes brownish black; after 15min, 500mL deionized water and 30mL H at 75-95 deg.C are added2O2To remove excess oxidant; obtaining golden yellow suspension;
(2) equally dividing the suspension into centrifugal tubes, and separating the suspension by using a centrifugal machine at the rotating speed of 3000 plus 5000 revolutions to obtain a brownish red precipitate; centrifugally cleaning the precipitate for 2 times by using a dilute hydrochloric acid solution, and washing the precipitate to be neutral by water; dispersing the precipitate in water, treating the obtained suspension liquid by using a cell disruptor for 5 minutes, carrying out water bath ultrasound for 2 hours, centrifuging to obtain supernatant, and freeze-drying to obtain dry graphene oxide powder;
(3) weighing the obtained 80mg of graphene oxide, putting the graphene oxide into a beaker, adding deionized water to prepare 200ml of solution, adding 0.05-0.1mol of diamine monomer cross-linking agent, uniformly stirring, placing the mixture into a water bath kettle at the temperature of 60 ℃, and continuously stirring for 6-12 hours to ensure that the graphene oxide and the cross-linking agent are fully subjected to cross-linking reaction;
(4) diluting the crosslinked suspension to 10mg/L by using deionized water, and passing through a mixed cellulose membrane or a cellulose acetate membrane serving as a filter in a vacuum filtration device under the fixed pressure of 0.1MPa to realize the self-assembly of the membrane, so as to obtain a modified graphene oxide composite membrane on the mixed cellulose membrane or the cellulose acetate membrane; and placing the composite membrane in a 60 ℃ oven for 6 hours to promote the crosslinking reaction between the graphene oxide and the monomer, and then soaking the composite membrane in pure water for 24 hours to remove physical adhesion substances and redundant crosslinking agents, thereby obtaining the target seawater purification membrane.
The reaction conditions are optimal reaction conditions;
according to the preparation method, the composite membrane is finally obtained by taking a mixed cellulose membrane or a cellulose acetate membrane as a lower support membrane, and the modified graphene oxide composite membrane on the support membrane is obtained through self-assembly of the membrane, wherein the support membrane can improve the strength of the whole composite membrane, so that the composite membrane is guaranteed to bear certain pressure intensity without being damaged during filtration, and the modified graphene oxide membrane mainly plays a role in filtering salt ions and desalting;
in the preparation method, the composite membrane is subjected to a crosslinking reaction between graphene oxide and a monomer at the temperature of 60-80 ℃, so that the composite membrane can promote the bonding strength of the support membrane and the modified graphene oxide membrane, improve the structural stability of the composite membrane, be better used in water flow and prolong the service life of the composite membrane in addition to the crosslinking reaction;
in conclusion, the graphene oxide composite membrane is modified by adopting three diamine monomers with different structures, the interlayer spacing of the nanosheets is adjusted and controlled to prevent GO from interlayer expansion in water, and then the GO is self-assembled on a mixed cellulose membrane or a cellulose acetate membrane to finally obtain the modified graphene oxide composite membrane.
The specific implementation mode is as follows:
in the following examples, except for specific description, the process is carried out by using the prior art, and the concentrated sulfuric acid is 98 wt% concentrated sulfuric acid.
Example 1
A preparation method of a seawater desalination membrane comprises the following specific steps:
(1) measuring 60mL of concentrated sulfuric acid in a beaker, placing the beaker in a water bath, cooling with ice water and continuously stirring, adding 0.5-1.5g of graphite powder and 0.5-1.5g of NaNO3Slowly adding 6-15g KMnO at the temperature below 10 DEG C4Keeping the mixture at 0 ℃ for 12-24h to promote low-temperature intercalation reaction, then placing the mixture in a constant-temperature water bath at 25-35 ℃ and keeping stirring; taking out after 20-40min, cooling to normal temperature, diluting with 150-180mL deionized water, stirring continuously until the system becomes brownish black, adding 500mL deionized water and 30mL H at 75-95 deg.C after 15min2O2To remove excess oxidant, it was observed that a large number of bubbles were generated in the system, while the liquid was simultaneously in the liquid stateThe black color is obviously changed into the golden yellow color of the graphite oxide, and a golden yellow turbid liquid is finally obtained;
(2) equally distributing the turbid liquid in a centrifugal tube, separating the turbid liquid by using a centrifugal machine at the rotating speed of 3000 plus 5000 revolutions to obtain a brownish red precipitate, centrifugally cleaning the precipitate for 2 times by using a dilute hydrochloric acid solution, and washing the precipitate to be neutral by water; dispersing the precipitate in water, treating the suspension with a cell disruptor for 5 minutes, performing ultrasonic treatment in a water bath for 2 hours, centrifuging to obtain a supernatant, and freeze-drying to obtain dry GO powder;
(3) weighing 60mg of GO, putting the GO into a beaker, adding deionized water to prepare 200ml of solution, adding 3-6g of ethylenediamine, uniformly stirring, putting the mixture into a water bath kettle at the temperature of 60 ℃, and continuously stirring for 6-12 hours to ensure that the GO and a cross-linking agent are fully subjected to a cross-linking reaction;
(4) diluting the suspension to 10mg/L, and passing through a mixed cellulose membrane or a cellulose acetate membrane used as a filter in a vacuum filtration device under a fixed pressure of 0.1MPa to realize self-assembly of the membrane, thereby obtaining a modified GO composite membrane on the mixed cellulose membrane or the cellulose acetate membrane; and placing the composite membrane in a 60 ℃ oven for 6-12h to promote the crosslinking reaction between GO and the monomer, and then soaking the composite membrane in pure water for 12-24h to remove physical adhesion substances and redundant crosslinking agents, thereby obtaining the target seawater purification membrane.
And (3) performance testing:
respectively selecting 0.05mol/L aCl and CaCl2Filtering the solution through a prepared GO-ethylenediamine composite membrane under the fixed pressure of 0.1MPa, wherein the highest water flow rate of the composite membrane is 20.55L/m2h.Bar, for Na+And Ca2+The maximum salt rejection of (a) was 19% and 26%, respectively.
Using a literature report [1]Nan Q,Li P,Cao B.Fabrication of positively charged nanofiltration membrane via the layer-by-layer assembly of graphene oxide and polyethylenimine for desalination[J]Applied Surface Science,2016,387:521-]Water flow rate results of the film of (2) (8.2L/m)2H · Bar), the maximum water flow rate of the composite membrane of the present application is greatly improved, and the salt rejection of the membrane is substantially equal to that of the literature.
It can be seen that the composite membrane structure that this application provided is strong, can adapt to higher processing speed, under the prerequisite of guaranteeing the desalination, has promoted the efficiency that the sea water purified greatly.
Example 2
A preparation method of a seawater desalination membrane comprises the following specific steps:
(1) measuring 100mL of concentrated sulfuric acid in a beaker, placing the beaker in a water bath, cooling with ice water and continuously stirring, and adding 1.5-5g of graphite powder and 1.5-3g of NaNO3Slowly adding 15-20g KMnO at the temperature below 10 DEG C4Keeping the mixture at 0 ℃ for 24-36H to promote low-temperature intercalation reaction, then placing the mixture in 35-45 ℃ constant-temperature water bath, keeping stirring, taking out the mixture after 40min, cooling to normal temperature, diluting the mixture with 150-180mL deionized water, continuously stirring the mixture until the system becomes brownish black, and adding 500mL deionized water and 30mL H at 75-95 ℃ after 15min2O2Removing excessive oxidant, observing that a large number of bubbles are generated in the system, and simultaneously, obviously changing the liquid from brown black into golden yellow of graphite oxide to finally obtain golden yellow turbid liquid;
(2) and equally dividing the turbid liquid into centrifugal tubes, and separating the turbid liquid by using a centrifugal machine at the rotating speed of 3000 plus 5000 revolutions to obtain a brownish red precipitate. Centrifuging and cleaning the precipitate with dilute hydrochloric acid solution for 2 times, washing with water to neutrality, dispersing the precipitate in water, treating the suspension with a cell disruptor for 5 minutes, performing ultrasonic treatment in water bath for 2 hours, centrifuging to obtain supernatant, and freeze-drying to obtain dried GO powder;
(3) weighing 100mgGO, putting into a beaker, adding deionized water to prepare 200ml of solution, adding 3-6g of urea, uniformly stirring, putting into a water bath kettle at the temperature of 60 ℃, and continuously stirring for 6-12h to ensure that the GO and a cross-linking agent are fully subjected to cross-linking reaction;
(4) diluting the suspension to 10mg/L, passing through a mixed cellulose membrane or a cellulose acetate membrane serving as a filter in a vacuum filtration device under a fixed pressure of 0.1MPa to realize self-assembly of the membrane, so as to obtain a modified GO composite membrane on the mixed cellulose membrane or the cellulose acetate membrane, placing the composite membrane in an oven at 80 ℃ for 12-24h to promote the crosslinking reaction between GO and a monomer, and then soaking the composite membrane in pure water for 12-24h to remove physical adhesive substances and redundant crosslinking agents, so that the target seawater purification membrane can be obtained.
And (3) performance testing:
respectively selecting 0.05mol/L NaCl and CaCl2Filtering the solution through the prepared GO-urea composite membrane under the fixed pressure of 0.1MPa, wherein the highest water flow rate of the composite membrane is 103.03L/m2h.Bar, for Na+And Ca2+The maximum salt rejection of (a) is 25.73% and 27.96%, respectively;
nanotechnology,2016,27(27):274002, was used as a report in the literature [2] Deng H, Sun P, Zhang Y, et al.
[3]Yuan Y,Gao X,Wei Y,et al.Enhanced desalination performance of carboxyl functionalized graphene oxide nanofiltration membranes[J].Desalination,2017,405:29-39.
[4]Ganesh B M,Isloor A M,Ismail A F.Enhanced hydrophilicity and salt rejection study of graphene oxide-polysulfone mixed matrix membrane[J]Disalination, 2013,313(7) 199-207. for comparison, the results are shown in comparison with literature reports [2]]The result of the composite membrane taking chitosan as a cross-linking agent on the NaCl solution water flow rate (15L/m)2Bar) is greatly improved, the cross-linking agent UR is better than chitosan in improving the water flow rate of the GO thin film, and the desalination rate of the composite membrane is greatly improved compared with the desalination rate result (17.4%) of NaCl solution of the composite membrane in document 2; and documents [3, 4 ]]Reported water flow rate results for GO-COOH and PSF/GO films (22.6L/m)2·h·Bar，24.5L/m2H · Bar) the maximum water flow rate of the composite membrane of the present application is greatly improved.
Example 3
A preparation method of a seawater desalination membrane comprises the following specific steps:
(1) measuring 80mL of concentrated sulfuric acid in a beaker, placing the beaker in a water bath, cooling with ice water and continuously stirring, and adding 0.5-2.5g of graphite powder and 1-1.5g of NaNO3Slowly adding 9-15g KMnO at the temperature below 10 DEG C4Keeping the temperature at 0 ℃ for 24h to promote low-temperature intercalation reaction,then placing the mixture in a constant temperature water bath at 35 ℃, keeping stirring, taking out the mixture after 30min, cooling the mixture to the normal temperature, diluting the mixture by using 180mL of 150-fold deionized water, continuously stirring the mixture until the system becomes brownish black, and adding 500mL of deionized water at 75-95 ℃ and 30mL of H after 15min2O2Removing excessive oxidant, observing that a large number of bubbles are generated in the system, and simultaneously, obviously changing the liquid from brown black into golden yellow of graphite oxide to finally obtain golden yellow turbid liquid;
(2) and equally dividing the turbid liquid into centrifugal tubes, and separating the turbid liquid by using a centrifugal machine at the rotating speed of 3000 plus 5000 revolutions to obtain a brownish red precipitate. Centrifuging and cleaning the precipitate with dilute hydrochloric acid solution for 2 times, washing with water to neutrality, dispersing the precipitate in water, treating the suspension with a cell disruptor for 5 minutes, performing ultrasonic treatment in water bath for 2 hours, centrifuging to obtain supernatant, and freeze-drying to obtain dried GO powder;
(3) weighing 80mg of GO, putting into a beaker, adding deionized water to prepare 200ml of solution, adding 5.4-10.8g of p-phenylenediamine, uniformly stirring, putting into a water bath kettle at the temperature of 60 ℃, and continuously stirring for 6-12 hours to ensure that the GO and a cross-linking agent are fully subjected to cross-linking reaction;
(4) diluting the suspension to 10mg/L, and passing through a mixed cellulose membrane or a cellulose acetate membrane used as a filter in a vacuum filtration device under a fixed pressure of 0.1MPa to realize self-assembly of the membrane, thereby obtaining a modified GO composite membrane on the mixed cellulose membrane or the cellulose acetate membrane. And placing the composite membrane in a 60 ℃ oven for 6 hours to promote the crosslinking reaction between GO and the monomer, and then soaking the composite membrane in pure water for 24 hours to remove physical adhesion substances and redundant crosslinking agents, thus obtaining the target seawater purification membrane.
And (3) performance testing:
respectively selecting 0.05mo/L NaCl and CaCl2Filtering the solution through the prepared GO-p-phenylenediamine composite membrane under the fixed pressure of 0.1MPa, wherein the highest water flow rate of the composite membrane is 113.03L/m2h.Bar, for Na+And Ca2+The maximum salt rejection of (a) was 12.83% and 20.81%, respectively.
The above-mentioned embodiments are intended to illustrate the technical solutions and advantages of the present invention, and it should be understood that the above-mentioned embodiments are only specific embodiments of the present invention, and are not intended to limit the present invention, and any modifications, additions, equivalents, etc. made within the scope of the principles of the present invention should be included in the scope of the present invention.
Claims (1)
1. A preparation method of a seawater desalination membrane is characterized by comprising the following steps: the sea water desalination membrane be modified graphene oxide complex film, specifically adopt the diamine monomer to modify graphene oxide, realize the regulation and control of nanometer piece interlamellar spacing in order to prevent GO from appearing the interlayer expansion in aqueous, later with its self-assembling on mixed cellulose membrane or cellulose acetate membrane, finally obtain modified graphene oxide complex film, concrete step is as follows:
(1) measuring 80mL of concentrated sulfuric acid in a beaker, placing the beaker in a water bath, cooling with ice water and continuously stirring, and adding 0.5-2.5g of graphite powder and 1-1.5g of NaNO3Slowly adding 9-15g KMnO at the temperature below 10 DEG C4Keeping the temperature at 0 ℃ for 24h to promote low-temperature intercalation reaction, then placing the mixture in a constant-temperature water bath at 35 ℃ and keeping stirring; after 30min, taking out and cooling to normal temperature, diluting with 150-180ml deionized water, and continuously stirring, wherein the system becomes brownish black; after 15min, 500mL deionized water and 30mL H at 75-95 deg.C are added2O2To remove excess oxidant; obtaining golden yellow suspension;
(2) equally dividing the suspension into centrifugal tubes, and separating the suspension by using a centrifugal machine at the rotating speed of 3000 plus 5000 revolutions to obtain a brownish red precipitate; centrifugally cleaning the precipitate for 2 times by using a dilute hydrochloric acid solution, and washing the precipitate to be neutral by water; dispersing the precipitate in water, treating the obtained suspension liquid by using a cell disruptor for 5 minutes, carrying out water bath ultrasound for 2 hours, centrifuging to obtain supernatant, and freeze-drying to obtain dry graphene oxide powder;
(3) weighing 80mg of graphene oxide obtained in the step (2), putting the graphene oxide into a beaker, adding deionized water to prepare 200ml of solution, adding 0.05-0.1mol of diamine monomer cross-linking agent, uniformly stirring, putting the mixture into a water bath kettle at the temperature of 60 ℃, and continuously stirring for 6-12 hours to fully perform cross-linking reaction on the graphene oxide and the cross-linking agent;
the diamine monomer is selected from urea;
(4) diluting the suspension subjected to crosslinking in the step (3) to 10mg/L by using deionized water, and passing through a mixed cellulose membrane or a cellulose acetate membrane serving as a filter in a vacuum filtration device under the fixed pressure of 0.1MPa to realize the self-assembly of the membrane, so as to obtain a modified graphene oxide composite membrane on the mixed cellulose membrane or the cellulose acetate membrane; and placing the composite membrane in a 60 ℃ oven for 6 hours to promote the crosslinking reaction between the graphene oxide and the monomer, and then soaking the composite membrane in pure water for 24 hours to remove physical adhesion substances and redundant crosslinking agents, thereby obtaining the target seawater purification membrane.
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| US20230201776A1 (en) * | 2020-05-14 | 2023-06-29 | Singapore University Of Technology And Design | A graphene oxide-based membrane |
| CN112604517B (en) * | 2020-11-26 | 2021-12-14 | 连云港鹏辰特种新材料有限公司 | Preparation of inorganic-organic composite gel membrane and application thereof in separation of hydrocarbon mixture |
| CN113307403B (en) * | 2021-05-26 | 2022-06-03 | 青岛科技大学 | Seawater desalination device |
| CN113877427A (en) * | 2021-10-14 | 2022-01-04 | 福建工程学院 | Preparation method of antibacterial and anti-fouling regenerated cellulose composite ultrafiltration membrane, composite ultrafiltration membrane and application |
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